DK2534719T3

DK2534719T3 - Rechargeable electrochemical cell

Info

Publication number: DK2534719T3
Application number: DK11702403.4T
Authority: DK
Inventors: Laurent Zinck; Christian Pszolla; Christiane Ripp; Markus Borck; Claudia Wollfarth
Original assignee: Alevo Int S A
Priority date: 2010-02-12
Filing date: 2011-02-04
Publication date: 2017-05-01
Also published as: EP3611788A1; ZA201206696B; HUE047163T2; RU2560717C2; EP3208869B1; HK1173267A1; WO2011098233A3; ES2617354T3; WO2011098233A2; HK1173854A1; US20110287304A1; KR101909084B1; DK3208869T3; US10892487B2; WO2011098232A1; RU2569328C2; EP2534719A2; KR20130006614A; IL221368A; KR20190128089A

Description

The invention relates to a rechargeable lithium battery cell having a positive electrode, a negative electrode and an electrolyte containing a conductive salt.

Rechargeable battery cells are of great importance in many technical fields. In many cases they are used for applications in which only relatively low currents are needed, such as in cell phones. There is also a large demand for battery cells for high-current applications. An important example are electrical drives for motor vehicles. The present invention is primarily directed to cells that are also suitable for high-current applications.

An important requirement is a high energy density. The cell should contain the largest possible amount of electrical energy per unit weight and volume. Lithium is particularly advantageous as an active metal in this respect.

In practice, rechargeable cells with a high energy density are almost exclusively lithium-ion cells. Their negative electrode is comprised of copper coated with carbon, into which lithium ions are inserted during charging. The positive electrode is also comprised of an insertion material, which is suitable for absorbing ions of the active metal. In general, the positive electrode is based on lithium cobalt oxide, which is coated on a current collector element made of aluminum. Both electrodes are very thin (thickness generally less than 100 m). During charging, the ions of the active metal are extracted from the positive electrode and inserted into the negative electrode. The reverse process takes place during discharge. Transport of the ions between the electrodes is performed by the electrolyte, which provides the required ion mobility. Lithium-ion cells contain an electrolyte consisting of a lithium salt (e.g. LiPF6) dissolved in an organic solvent or solvent mixture (e.g. based on ethylene carbonate). Said cells will hereafter also be referred to as “organic lithium-ion cells”.

Organic lithium-ion cells are problematic with respect to safety. Safety risks are posed in particular by the organic electrolyte. If a lithium-ion cell catches fire or even explodes, the organic solvent of the electrolyte forms the combustible material. In order to avoid such risks, it is necessary to take additional measures, particularly with respect to exact control of the charging and discharging processes and with respect to additional safety measures in battery construction. For example, the cell can contain components that melt in the event of a fault and flood the battery with molten plastic. However, these measures lead to increased costs and increase the volume and weight, thereby reducing the energy density.

The problems are particularly severe if battery cells are to be developed for high-current applications. The requirements with respect to stability and long-term operating safety are particularly high. The term “high-current cells” is used here to designate cells that (at nominal voltage) have a current carrying capacity referred to the electrode area (hereafter “ampacity per unit area”) of at least 10 mA/cm2, preferably at least 50 mA/cm2 and particularly preferably at least 150 mA/cm2.

There is a great need for improved rechargeable battery cells that meet in particular the following requirements:

Very good electrical power data, in particular high energy density and simultaneously high extractable currents (power density).

Safety, also under the difficult ambient conditions in a motor vehicle. Long service life, in particular a large number of useful charging and discharging cycles.

Lowest possible price, i.e. inexpensive materials and production methods with minimum complexity.

Other important requirements for practical operation such as overcharging capability and deep discharge capability.

The invention addresses the technical problem of making available a battery cell that - overall - meets these partly contradictory requirements better than known cells.

The technical problem is solved by an electrochemical rechargeable lithium battery cell according to claim 1.

Hereafter, the abbreviation “LIP” will be used for lithium iron phosphate.

In the context of the invention, the term "S02-based electrolyte" designates an electrolyte containing SO2 not just in low concentration as an additive, but in which the SO2 at least to some degree enables the mobility of the ions of the conductive salt contained in the electrolyte, thus ensuring the charge transport. The electrolyte is preferably essentially free of organic materials, whereby “essentially free” is to be construed such that the quantity of any organic materials present is so small that they do not represent any safety risk. Lithium cells with an S02-based electrolyte are hereafter referred to as L1-SO2 cells. S02-based electrolytes for lithium cells have been discussed for many years. In (1) “Handbook of Batteries”, David Linden (editor), 2nd edition, McGraw-Hill, 1994 the high ionic conductivity of an SC>2-based inorganic electrolyte is emphasized. It is stated that this electrolyte is also advantageous with respect to other electrical data. It is further stated therein that systems with an SC>2-based electrolyte have been under investigation for a long time and are still of interest for special applications, but that the further commercial applicability is limited, in particular since the electrolyte is toxic and highly corrosive. SO2 is sometimes used as an additional component of the electrolyte in organic lithium-ion cells. For instance, the document WO 2008/147751 A1 describes an electrochemical cell with an electrolyte that contains nitriles as solvent. By using these nitriles a lower viscosity, a lower melting point, a higher dielectric constant, a higher oxidation resistance, a high anodic stability and an increased longevity at high temperatures are to be achieved. In some embodiments of the cell described therein, SO2 is to used as an additive to improve the conductivity at low temperatures. A plurality of possible cathode materials, among them LIP, is mentioned.

Battery cells with SO2 electrolytes are described in the following documents, for example: (2) US Patent 5,213,914 (3) WO 00/44061 and US Patent 6,709,789 (4) WO 00/79631 and US Patent 6,730,441 (5) WO 2005/031908 and US 2007/0065714 (6) L. Zinck et al. "Purification process for an inorganic rechargeable lithium battery and new safety concepts", J. Appl. Electrochem., 2006,1291-1295 (7) WO 2008/058685 and US Patent Application 2010/0062341 (8) WO 2008/147751 and WO 2009/077140

In the exemplary embodiments described in these documents, the positive electrodes are always based on a lithium metal oxide, in particular based on lithium cobalt oxide.

Lithium metal phosphates have also been known for a long time as a positive electrode material for lithium-ion cells with organic electrolytes. Early experimental research is reported in (9) US Patent 5,910,382 (10) Padhi et al. "Phospho-olivines as Positive-Electrode Materials for Rechargeable Lithium Batteries", J. Electrochem. Soc., 1997, 1188-1194

In (9) and (10), cathode materials for lithium cells are studied that contain the polyanion (PO4)3'. The study refers to compounds with the metals Mn, Fe, Co and Ni that are present in two different structures, namely the olivine structure and the NASICON structure. The influence of the structures on the insertion of lithium is described and experiments with battery cells are reported herein in which a small number of charging cycles (maximum of 25 cycles) were performed. (9) and (10) also emphasize the problems that are associated with the use of LIP electrodes in lithium-ion cells. A cell voltage of only 3.5 V is described even for a very small ampacity per unit area of 0.05 mA/cm2. In comparison, the cell voltage with a lithium cobalt oxide electrode is 4 V and thus approximately 14 % higher. Furthermore, the electrical conductivity of the LIP is very poor. This leads to a significant decrease in the cell voltage even with relatively low current loads. The capacity of the cells also shows strong dependence on the current load and falls to values that make the cell essentially useless even with an ampacity per unit area of less than 0.2 mA/cm2.

According to (11) US Patent 7,338,734 these problems can be solved, in a lithium-ion cell with organic electrolyte, by enlarging the specific surface area of the active material of the positive electrode (in other words using a material consisting of very small particles) and using -instead of a pure lithium iron phosphate - a material that is doped with one of the elements of the groups II A, III A, IV A, V A, VIA and III B of the periodic system, in particular niobium.

Thus, significantly improved electrical data are achieved compared to previously known organic lithium-ion cells with a positive LIP electrode. However, manufacture of the cells is very complex, particularly due to the required doping of the LIP material, due to the production of very fine LIP fractions, due to the casting of thin (film-type) electrode layers and due to the assembly of the cells with the thin electrode layers.

In the context of the present invention it has been discovered that, surprisingly, very good electrical power data - also for high-current applications - can be achieved with substantially less time and effort by using a positive LIP electrode in an L1-SO2 cell according to claim 1. The invention allows to use lithium iron phosphate even without doping while still guaranteeing a high current carrying capacity. Moreover, it is not necessary to use an extremely fine-grain LIP. In the context of the invention, it has been found advantageous to use an LIP with a specific surface area of no more than 40 m2/g, measured according to the Brunauer-Emmett-Teller (BET) method. It is also possible to advantageously use materials with no more than 30 m2/g and even materials with no more than 15 m2/g. The preferred mean particle size is at least 0.2 pm. It is also possible to advantageously use materials with a mean particle size of at least 0.5 pm, at least 1 pm or even at least 2 pm.

The positive electrode according to the invention is preferably porous. However, the porosity should preferably not be too high. The following maximum values for porosity are particularly preferred in this order: 50 %, 45 %, 40 %, 35 %, 30 %, 25 %, 20 %.

During operation of the cell the pores of the positive electrode are preferably completely filled with electrolyte. Suitable conductive salts of the electrolyte are in particular aluminates, halogenides, oxalates, borates, phosphates, arsenates and gallates of an alkali metal or alkaline earth metal. In the context of the invention a lithium tetrahalogenoaluminate is preferably used, and particularly preferably a lithium tetrachloroaluminate.

The electrolyte preferably contains at least 2.0 mole SO2 per mole of conductive salt, the following values being further preferred in this order: at least 2.5 mole SO2 per mole of conductive salt, at least 3.0 mole SO2 per mole of conductive salt, at least 4.0 mole SO2 per mole of conductive salt. In the context of the invention it has been found that, surprisingly, an electrolyte with a relatively low concentration of conductive salt is advantageous, in particular with respect to stability over a large number of cycles, and in spite of the resultant higher vapor pressure. A cell according to the invention is particularly advantageous if the thickness of the positive electrode is at least 0.25 mm, preferably at least 0.3 mm, further preferably at least 0.4 mm, further preferably at least 0.5 mm and particularly preferably at least 0.6 mm. The quantity of active material per unit area of the positive electrode (“loading”) should also be high. It is preferably at least 30 mg/cm2, the following minimum values being more preferred in this order: 40 mg/cm2, 60 mg/cm2, 80 mg/cm2,100 mg/cm2,120 mg/cm2 and 140 mg/cm2.

Significant advantages are associated with the large thickness of the positive electrode and the correspondingly high loading with active material. In particular, the capacity referred to the area of the positive electrode ("capacity per unit area") is very high. The theoretical capacity of LIP is 169 mAh/g. In experimental testing of the invention, it has been found that this theoretical value is achieved in very good approximation (more than 90 %) in an U-SO2 cell. The capacity per unit area of the positive electrode is preferably at least 5 mAh/cm2, the following minimum values being even more preferred in this order: 7.5 mAh/cm2,10 mAh/cm2, 12.5 mAh/cm2, 15 mAh/cm2, 20 mAh/cm2, 25 mAh/cm2.

In the context of the invention it has been found that by combining an LIP electrode and an S02-based electrolyte it is possible to manufacture an electrochemical battery cell that is significantly improved with respect to the combined requirements described above, said cells being particularly suitable for applications related to electromobility (battery and hybrid vehicles, for example):

The high loading of the positive electrode and the resultant high capacity per unit area allow production of cells that have a high total capacity and at the same time a relatively small electrode area. The loading can significantly exceed the minimum values stated above and reach a value of more than 100 mg/cm2. An area of only 60 cm2 is then sufficient for a capacity of 1 Ah. The required electrode area is smaller by a factor of 3 than that of conventional LIP electrodes described for organic lithium-ion cells, which have a thickness of 50 to 90 pm and a loading per unit area of 4 to 6 mAh/cm2, and which consequently require a total electrode area of 170 to 250 cm2 to provide a capacity of 1 Ah. As a result of the reduced area of the positive electrode, the areas of the separator and of the negative electrode are also reduced. Furthermore, for example in the case of prismatic cells with a plurality of electrodes, a smaller number of current collector tabs is required for connection with the cell terminals. Also interconnection of the electrodes in the housing is much simpler with a small number of electrodes.

The current carrying capacity is very high. Positive electrodes according to the invention are able to provide an ampacity per unit area of 300 mA/cm2, for example.

At least 90 % of the theoretical capacity of the positive electrode can be used in practice. This means that the lithium ions can be extracted almost completely from the positive electrode during charging and inserted into the positive electrode again during discharging. The invention also allows to achieve good values with respect to the dependence of the capacity on the current carrying capacity. In other words, a large part of the original capacity of the cell is still available with a high current load. Overall, during the service life of the cell, the practically useful capacity of the cell according to the invention is higher than with a lithium cobalt oxide electrode, although the theoretical capacity of the LIP is only 60 % in comparison with lithium cobalt oxide.

The high number of charging and discharging cycles required for electromobility applications is possible. More than 9,000 full cycles were achieved in experimental testing.

It is not necessary to regenerate the electrolyte by overcharging the cell, such as described in document (8), for example. Consequently, the coulometric efficiency is increased. However, the cell according to the invention is capable of overcharging if this is required in a specific application.

The self-discharge of the cell according to the invention is exceptionally low. It can therefore be stored for a long period in charged condition and used immediately without renewed charging. Furthermore, the safety risk of “thermal runway” associated with self-discharge, as described in document (2) for example, is eliminated.

The stability of a negative carbon electrode, as preferably used in the context of the invention, is significantly improved. The negative electrode can even be manufactured without a binding agent.

It is not necessary to use a relatively high share of carbon-based conductivity-improving material in the active material of the positive electrode, as described in documents (9), (10) and (11). Rather, relatively small quantities of conductivity-improving material are sufficient. The carbon content of the positive electrode is preferably less than 10 wt.%, the following maximum values being further preferred in this order: 7 wt.%, 5 wt.%, 2 wt.%.

The share of binding agent can also be very low. The positive electrode preferably contains no more than 10 % binding agent, the following maximum values being further preferred in this order: 7 wt.%, 5 wt.%, 2 wt.%.

On the basis of the information available prior to the invention, it could not be expected that an L1-SO2 cell with LIP as the active material of the positive electrode would be functional and even particularly advantageous.

As mentioned, the cell voltage of a lithium-ion cell with LIP is almost 15 % lower than the cell voltage of a lithium-ion cell with lithium cobalt oxide. Consequently, a correspondingly lower value of the energy density was to be expected.

The previously published documents on L1-SO2 cells described a positive electrode based on an oxide, particularly lithium cobalt oxide, as being ideal in combination with the SO2 electrolyte. In document (5), an activating cleaning process was recommended to improve the electrode properties.

The electrodes are in contact with the electrolyte in the cell and can therefore react primarily only with the electrolyte. The electrolyte is therefore decisive for possible reactions of the materials contained in the electrodes. A problematic characteristic of an S02-based electrolyte, as already described in document (1), is its high level of corrosiveness. The chemical behavior of LIP in an organic electrolyte does not tell anything about its chemical resistance in a fundamentally different SC>2-based inorganic electrolyte. Since lithium cobalt oxide had proven itself in an U-SO2 cell, alternatives were sought, if at all, in chemically related oxide compounds.

Good conductivity was seen as being the most important advantage of an S02-based electrolyte. On the other hand, it was known that LIP is a very poorly conducting electrode material. On this basis it seemed illogical, when developing a battery cell suitable also for high-current applications, to combine an electrolyte that is advantageous with respect to the internal resistance of the cell with an electrode material that is obviously disadvantageous in this regard.

It is already mentioned in document (1) that the selection of positive electrode materials for an L1-SO2 cell is restricted to such compounds that are reduced at potentials above the reduction potential of SO2. Since the reduction potential of LIP (2.9 V) is considerably lower than that of lithium cobalt oxide (3.5 V), there remains only a narrow voltage range in which the cell should be, preferably completely, charged and discharged. When testing the LIP in an organic cell according to documents (9) and (10), only about 60 % of the lithium was extracted from the LIP, although charging and discharging took place with an extremely low ampacity per unit area of 50 μΑ/cm2.

Both the LIP-based positive electrode and the carbon-based negative electrode are intercalation electrodes operating by insertion of the active metal lithium in their grid structure during charging and discharging. A preferred embodiment of the invention relates to such intercalation electrodes, and generally also to other insertion electrodes that are suitable for taking up lithium internally. According to this embodiment, at least one of the electrodes in battery cells with an S02-based electrolyte is an insertion electrode suitable for taking in lithium ions, said electrode being pretreated to reduce the covering layers. Such an embodiment is advantageous for the above-described rechargeable lithium battery cell with a positive LIP electrode, but is also of significance for all insertion electrodes in an S02-based electrolyte.

The cover-layer-reduction pretreatment relates to the formation of covering layers on the surface of insertion electrodes during the initial charging cycles. Covering layer formation does not just consume charging current, but also leads to an irreversible consumption of active components of the battery system and thus to a reduction in capacity for the remaining battery service life. The capacity loss associated with covering layer formation is reduced by the cover-layer-reduction pretreatment.

The invention is illustrated in more detail hereafter on the basis of the figures. The technical features shown and described therein can be used individually or in combination to create preferred embodiments of the invention. In the figures: FIG. 1 shows a cross-sectional view of a battery cell according to the invention; FIG. 2 shows a cross-sectional view of a metal foam suitable for the invention; FIG. 3 shows a cross-sectional view of a positive electrode; FIG. 4 shows the dependence of the discharge capacity on the number of cycles for an experiment performed with a positive electrode; FIG. 5 shows the dependence of the discharge capacity on the discharge rate for an experiment performed with a positive electrode in comparison with published results; FIG. 6 shows the dependence of the electrical resistance of an electrode on the number of cycles for an experiment performed with a positive electrode; FIG. 7 shows the dependence of the capacity on the number of cycles for an experiment performed with two different positive electrodes; FIG. 8 shows the dependence of the capacity on the number of cycles for a further experiment performed with two different positive electrodes; FIG. 9 shows the dependence of the discharge capacity on the number of cycles for an experiment performed with two different cells; FIG. 10 shows the dependence of the capacity on the number of cycles for a long-duration experiment; FIG. 11 shows the dependence of the electrical voltage on the charging capacity for three differently pretreated negative electrodes.

The housing 1 of the rechargeable battery cell 2 shown in FIG. 1 encloses an electrode arrangement 3 comprising a plurality (three in the case shown) of positive electrodes 4 and a plurality (four in the case shown) of negative electrodes 5. The electrodes 4, 5 are connected in the usual manner with corresponding terminal contacts 9, 10 of the battery by means of electrode leads 6, 7. The cell is filled with an S02-based electrolyte, not shown in the figures, in such a manner that the electrolyte preferably penetrates completely into all pores, particularly inside the electrodes 4, 5.

As is common, the electrodes 4, 5 have a planar shape, i.e. they are shaped as layers having a thickness which is small relative to their extension in the other two dimensions. They are separated from each other by separators 11. The housing 1 of the prismatic cell shown is essentially cuboid, the electrodes and the walls shown in cross-section in FIG. 1 extending perpendicularly to the drawing plane and being essentially straight and flat. However, the cell according to the invention can also be designed as a spirally wound cell.

As is common, the electrodes 4, 5 comprise a current collector element, which is made of metal and serves to provide the required electronically conductive connection of the active material of the respective electrode. The current collector element is in contact with the active material involved in the electrode reaction of the respective electrode. The current collector element of the positive electrode, preferably also the current collector element of the negative electrode, is provided in the form of a three-dimensional porous metal structure, particularly in the form of a metal foam. In this context, the term “three-dimensional porous metal structure” designates every structure made of metal that does not just extend like a thin sheet only over the length and width of the planar electrode, but also extends over its thickness dimension, and which is porous in such a manner that the active material of the electrode can be incorporated into the pores. FIG. 2 shows an electron microscope image of a cross-section of a metal foam structure suitable for the invention. On the basis of the indicated scale, it is evident that the pores P have on average a diameter of more than 100 pm and thus are relatively large. Instead of the metal foam, it is also possible to use a different three-dimensional metal structure, for example in the form of a metal fleece or metal fabric.

During manufacture of the electrode, the LIP material is incorporated into the porous structure of the current collector element such that it fills the pores of the current collector element uniformly over the whole thickness of the metal structure. The material is then pressed under high pressure, the thickness after the pressing operation being preferably no more than 50 %, particularly preferably no more than 40 %, of the initial thickness.

The resultant electrode structure is shown in FIG. 3, again in the form of an electron microscope image. The electrode material was cooled in liquid nitrogen and then broken, because a cutting operation would have corrupted the structural features. In spite of certain material damage caused by breaking, the primary features of the structure of a positive electrode according to the invention are clearly visible in FIG. 3.

The electrode is very thick in comparison with known LIP electrodes. In the example shown here, the thickness d is approximately 0.6 mm. The three-dimensional porous metal structure 13 of the current collector element extends essentially over the whole thickness d of the current collector element and the active LIP material 15 is distributed essentially homogeneously therein. With respect to the two stated conditions, "essentially" is to be construed such that the cell function is only slightly impaired by any deviations. In any case, the porous metal structure should extend over at least 70 %, preferably at least approximately 80 %, of the thickness of the electrode.

The positive electrode contains a binding agent to improve its mechanical strength. In the context of the invention, fluorinated binding agents, in particular THV (terpolymer of tetrafluoroethylene, hexafluoropropylene and vinylidene fluoride) and PVDF (polyvinylidene fluoride), have proven suitable. Advantageously, it is sufficient if the binding agent is contained in the electrode in a relatively low concentration.

The negative electrode contains as active material preferably carbon in a form suitable as insertion material for taking in lithium ions. The structure is preferably similar to that of the positive electrode with the following features:

For the negative electrode also, the current collector element preferably has a three-dimensional porous metal structure, in particular in the form of a metal foam.

It is relatively thick, having a thickness of at least 0.2 mm, the following values being further preferred in this order: 0.3 mm, 0.4 mm, 0.5 mm, 0.6 mm.

The quantity of active material of the negative electrode per unit area is at least 10 mg/cm2, the following values being further preferred in this order: 20 mg/cm2, 40 mg/cm2, 60 mg/cm2, 80 mg/cm2, 100 mg/cm2.

The capacity per unit area is preferably at least 2.5 mAh/cm2, the following values being further preferred in this order: 5 mAh/cm2, 10 mAh/cm2, 15 mAh/cm2, 20 mAh/cm2, 25 mAh/cm2, 30 mAh/cm2.

It is preferably porous, having a porosity of no more than 50 %, the following values being further preferred in this order: 45 %, 40 %, 35 %, 30 %.

The binding agent proportion is preferably no more than 5 wt.%, further preferably no more than 3 wt.% and particularly preferably no more than 1 wt.%. A negative electrode that does not contain any binding agent is particularly preferred.

Further information on the invention and its preferred embodiments is provided on the basis of the experiments described below.

Experiment 1: A paste was produced using the following components: 94 wt.% undoped lithium iron phosphate with carbon surface coating; mean particle size approx. 2 - 3 pm 2 wt.% carbon black as conductivity agent 4 wt.% THV as binding agent,

First the binding agent was dissolved in acetone, then carbon black was added to the solution while stirring, and finally the active mass was added alternately with further solvent, also while stirring.

The paste was incorporated homogeneously into a metal foam having an initial porosity of more than 90 %, and dried for an hour at 50 °C. After cooling, the electrode material was pressed by means of a calender to a thickness of 0.6 mm, starting from an initial thickness of 1.6 mm. It was then subjected to a tempering process at 180 °C. The resultant electrode material had a cross-section corresponding to FIG. 3.

Pieces with a size of 1 cm2 were cut out of the electrode material. The pieces had a capacity of approx. 13 mAh. They were then examined in an E-cell with a three-electrode arrangement, in which the reference and counter electrodes were made of metallic lithium. The electrolyte used in the E-cell had the composition LiAICU * 1.5 SO2.

In order to determine the discharge capacities of the electrodes for different current loads, 40 charging and discharging cycles were performed in the E-cells. Charging took place in each case with the same charging rate of 1 C (“C” indicates a factor of the nominal capacity charged or discharged in one hour). Discharging took place after each charging operation, with the cells being discharged at the following rates in the 40 cycles:

10 cycles 1 C 4 cycles each 2 C, 4 C, 8 C, 10 C, 15 C 10 cycles 1 C.

Charging took place up to a voltage of 3.7 V. Discharging ended at a voltage of 3.2 V. FIG. 4 shows, as mean values over eight experiments, the discharge capacity Qd in mAh/g as a function of the cycle number. It is evident from the figure that a large share of the nominal capacity is still available even with very high discharge rates. If, for example, the cell is discharged with such a high current that it is empty in six minutes (10 C), it is still possible to extract two thirds of the nominal capacity. FIG. 5 summarizes the results illustrated in FIG. 4, showing the discharge capacity Qd as a function of the discharge rate C (graph A). Graph B shows values from the publication (12) W. Porcher et al., "Design of Aqueous Processed Thick LiFeP04 Composite Electrodes for High-Energy Lithium Battery, J. Electrochem. Soc., 2009, A133-A144

This publication describes the production of relatively thick electrodes for organic lithium-ion cells. Here a thickness of 0.2 mm is already considered as thick (in comparison with previously usual thicknesses). The electrodes are manufactured with a water-soluble binding agent in aqueous suspension. The resulting capacity per unit area (“capacity density”) is specified as 3 mAh/cm2, with loading of 20 mg/cm2 and an electrode thickness of 200 m. The measurement data plotted in FIG. 5 was taken from FIG. 1 on Page A135 of the publication for their best material (“CMC”). It is evident that the capacity decreases with the discharge rate much faster than for the electrode according to the invention. For a discharge rate of 10 C, for example, the positive electrode described in the publication for an organic lithium-ion cell has a discharge capacity of 18 mAh/g compared with 100 mAh/g for the present invention. The comparison is summarized by the following Table 1:

Table 1:

FIG. 6 shows the values for the resistance R of the electrode that were measured on the E-cells after charging, as a function of the cycle number. In spite of the very high discharge rates, the resistance of the electrode remains largely stable in the range between 0.6 and 0.8 ohms.

Experiment 2:

For this experiment, a spirally wound cell of the type Sub-C was produced, the electrodes having a capacity of 17 mAh/cm2 (positive electrode with LIP mass as for experiment 1).

The electrodes were wound into a spiral together with a separator positioned between them and placed in the Sub-C housing. This was then filled with an electrolyte solution with the composition LiAICU*6S02.

The cell was charged with a charging rate of 0.7 C to 831 mAh. The discharge current was 10 A, corresponding to a discharge rate of 7 C. Discharging was stopped at a cell voltage of 2 V and with an extracted capacity of 728 mAh. This corresponds to 88 % of the charged capacity. It was thus possible to prove the high current-carrying capacity.

Experiment 3:

Using a positive electrode according to the invention and a positive electrode containing lithium cobalt oxide as the active material, but otherwise having the same features, the dependence of the capacity on the number of charging and discharging cycles (each with 1 C) in an E-cell was determined. FIG. 7 shows the results obtained using an SO2 electrolyte containing 1.5 mole SO2 per mole of conductive salt (lithium tetrachloroaluminate). The discharge capacity Qd in percent of the theoretical value is plotted against the number of charging and discharging cycles performed, where graph A relates to the LIP electrode and graph B to the lithium cobalt oxide electrode. It is evident that almost the entire theoretical capacity can be practically used with the LIP electrode, whereas on average only around 60 % of the theoretical capacity is available in practice for the comparison electrode. This essentially compensates for the higher theoretical capacity of the lithium cobalt oxide (273 mAh/g) in comparison with the LIP (170 mAh/g). FIG. 8 shows the results of an experiment that differed from the experiment that served as a basis for FIG. 7 only with respect to the concentration of the conductive salt in the electrolyte. In this case it was 4.5 mole SO2 per mole of LiAICU. It is evident that the LIP electrode behaves very well also in the electrolyte containing a lower conductive salt concentration (graph A), whereas the capacity for the lithium cobalt oxide electrode rapidly falls to unacceptably low values (graph B).

Experiment 4: FIG. 9 shows the results of an experiment in which the function of a complete cell with a negative carbon electrode, an SO2 electrolyte, and a positive electrode according to the invention with a capacity of 19 mAh/cm2 (graph A) was compared with a cell with a positive electrode based on lithium cobalt oxide (graph B), but otherwise having the same features. In this case, the electrolyte contained 6 mole of SO2 per mole LiAICL.

The discharge capacity Qd in percent of the nominal value is plotted against the number of cycles. After an initial decrease, the extractable capacity for the cell according to the invention is almost constant, whereas it rapidly decreases to unacceptably low values for the comparison cell. This confirms the superiority of the cell according to the invention, in particular in combination with an electrolyte containing a relatively high SO2 proportion.

Overall, it was found in the context of the invention that it is advantageous to use an electrolyte with a relatively low conductive salt content relative to the quantity of SO2. This contradicts the recommendations predominantly given in the prior publications on lithium-S02 cells, to use an electrolyte with a relatively low SO2 proportion, in particular with regard to the vapor pressure. A means to improve the capacity stability of the cell which can be used alternatively or additionally to the high SO2 content, is the addition of a lithium halogenide, preferably a lithium chloride, this salt being contained preferably as an admixture in the active mass of the positive electrode. FIG. 10 shows the results of a long-duration test with a cell as for FIG. 9, graph A, where the extracted capacity Qd is again plotted against the number of cycles.

The figure shows approx. 9,700 cycles, in which the reduction in the extractable capacity per 100 cycles is exceptionally low, namely less than 0.4 %.

Cover-layer-reducing petreatment:

As described above, it is possible to improve the capacity stability of lithium-SC>2-cells with at least one insertion electrode, particularly an intercalation electrode, by means of a pretreatment to reduce covering layers on at least one insertion electrode. There are various possibilities to this end. A first possibility is to subject the insertion electrode to a temperature treatment. This applies in particular for carbon electrodes, which are tempered at a temperature of at least 900 °C under exclusion of oxygen (preferably under inert gas) for a long time (at least 10, preferably at least 20 and particularly preferably at least 40 hours).

Alternatively or additionally, the formation of covering layers on a negative carbon electrode can be reduced by using a graphite material with a relatively low specific surface area.

According to a further preferred embodiment, the pretreatment to reduce the covering layers comprises providing the corresponding electrode with a thin surface coating.

Such a surface coating can be effected in particular by means of atomic layer deposition. This method has been used in recent times for numerous purposes. An overview is given, for example, in the publication (13) S. M. George "Atomic Layer Deposition: An Overview", Chem. Rev. 2010, 111-131

The process parameters should be adapted to the requirements of the electrode. In the context of the invention, it was found that particular advantages are ob tained if the carbon electrode is pretreated with NO2-TMA (nitrogen dioxide-tri-methylaluminum). This seeds an initial functional layer on the carbon, this layer being advantageous for subsequent ALD treatment. In this context, reference can additionally be made to (14) G. M. Sundaram et al. "Leading Edge Atomic Layer Deposition Applications", ECS Transactions, 2008,19-27

Preferably coating by ALD refers to a thin layer of AI2O3. According to current knowledge, S1O2 is a suitable alternative. A further possibility for applying a surface coating suitable for reducing the covering layers is dip coating. To this end, either the insertion active material intended for processing in the electrode or the whole electrode is brought into contact with a reaction solution that contains starting materials suitable for the formation of the layer. A temperature treatment is then performed to form and harden the layer. The following method can be used, for example:

Isopropanol, water, 1 molar hydrochloric acid and tetraethylorthosilicate are mixed in a mole ratio of 3:1:1:1. The solution is kept at room temperature. It is then diluted with isopropanol in the volume ratio 1:1. The electrodes to be treated are dipped in the reaction solution for 30 seconds or, if bubble formation is observed, until bubble formation has stopped. The electrodes are then dried in a drying cabinet at 200 °C without vacuum for 48 hours. FIG. 11 shows the results of an experiment with the following electrode materials: A negative electrode without cover-layer-reducing pretreatment B negative electrode where the active material was pretreated by means of dip coating with formation of an S1O2 layer, before incorporation into the electrode C negative electrode that was pretreated as a whole by means of dip coating with formation of an S1O2 layer.

The three experimental electrodes were examined in an E-cell. During charging of the electrode, the voltage U against lithium was plotted in volts against the charge state Q, as fraction of the nominal capacity Qn. The three graph groups illustrated show the results of several experiments in each case with the above-described electrodes. In FIG. 11, the area below the graph corresponds to the cell capacity lost due to covering layer formation. It is evident that the capacity loss for the two pretreated electrodes is significantly less than for the untreated electrode, the electrode pretreated in its entirety being slightly better than the other pretreated electrode.

Claims

A rechargeable lithium battery cell with a housing, a positive electrode, a negative electrode and an electrolyte containing a conducting salt, wherein the electrolyte is based on SO2, the positive electrode comprises a conductor element with a three-dimensional porous metal structure, and the positive electrode contains LiFePCU as active material.

Battery cell according to the preceding claim, characterized in that the positive electrode is at least 0.25 mm, preferably at least 0.3 mm, further preferably at least 0.4 mm, and further preferably at least 0.5 mm and more preferably at least 0 mm. , 6 mm thick.

Battery cell according to one of the preceding claims, characterized in that the positive electrode, in relation to its surface, contains at least 30 mg / cm2, preferably at least 40 mg / cm2, further preferably at least 60 mg / cm2, further preferably at least 80 mg / cm 2, further preferably at least 100 mg / cm 2, further preferably at least 120 mg / cm 2, and more preferably at least 140 mg / cm 2 of active material.

Battery cell according to one of the preceding claims, characterized in that the positive electrode is porous, wherein the porosity of the positive electrode is preferably at most 50%, further preferably at most 45%, further preferably at most 40%, further preferably at most 35%, further preferably at most 30%, further preferably at most 25% and especially preferably at most 20%.

Battery cell according to one of the preceding claims, characterized in that the three-dimensional porous metal structure is formed as metal foam.

Battery cell according to claim 1, characterized in that the porous metal structure extends substantially over the entire thickness of the positive electrode.

Battery cell according to one of claims 1 to 6, characterized in that the active material in the positive metal structure is substantially homogeneously distributed.

Battery cell according to one of the preceding claims, characterized in that the negative electrode is 0.2 mm, preferably at least 0.3 mm, further preferably at least 0.4 mm, and further preferably at least 0.5 mm and most preferably at least 0.6 mm thick.

Battery cell according to one of the preceding claims, characterized in that the positive electrode contains a binder, preferably a fluorinated binder, in particular a polyvinylidene fluoride and / or a terpolymer of tetrafluoroethylene, hexafluoropropylene and vinylidene fluoride, preferably at a concentration of at most 10. % by weight, further preferably at a concentration of not more than 7% by weight, further preferably at a concentration of not more than 5% by weight, and more preferably preferably at a concentration of not more than 2% by weight.

Battery cell according to one of the preceding claims, characterized in that the negative electrode contains carbon for the absorption of lithium ions.

Battery cell according to one of the preceding claims, characterized in that the amount of the active material in the negative electrode, relative to its surface, is at least 10 mg / cm 2, preferably at least 20 mg / cm 2, further preferably at least 40 mg. / cm 2, further preferably at least 60 mg / cm 2, further preferably at least 80 mg / cm 2, and more preferably at least 100 mg / cm 2.

Battery cell according to one of the preceding claims, characterized in that the negative electrode is porous and its porosity is at most 50%, further preferably at most 45%, further preferably at most 40%, further preferably at most 35% and especially preferably at most 30%. .

Battery cell according to one of the preceding claims, characterized in that the negative electrode contains a binder, preferably a fluorinated binder, in particular a polyvinylidene fluoride and / or a terpolymer of tetrafluoroethylene, hexafluoropropylene and vinylidene fluoride, preferably at a concentration of not more than 5. % by weight, further preferably at a concentration of at most 3% by weight, and most preferably at most at most 1% by weight.

Battery cell according to one of the preceding claims, characterized in that the electrolyte contains at least 2 moles of SO2, preferably at least 2.5 moles of SO2, further preferably at least 3 moles of SO2 and most preferably at least 4 moles of SO2 per mole of lead salt.

Battery cell according to one of the preceding claims, characterized in that the electrolyte as a guide salt contains a halide, oxalate, borate, phosphate, arsenate or gallate, preferably a lithium tetrahalo aluminate, especially preferably a lithium tetrachloro aluminate.

Battery cell according to one of the preceding claims, characterized in that the cell has a current load capacity, relative to the surface of the positive electrode, of at least 10 mA / cm2, preferably at least 50 mA / cm2 and most preferably at least 150 mA / cm2.

Battery cell according to one of the preceding claims, characterized in that it contains a lithium halide, preferably lithium chloride, preferably mixed with the active metal of the positive electrode.

Battery cell according to one of the preceding claims, characterized in that at least one of the electrodes is an insertion electrode suitable for recording lithium ions, the active material of which is a coating layer reducing pre-treated.

Battery cell according to claim 18, characterized in that the at least one electrode is surface-coating reducing by a coating of the active material of the electrode, the surface coating being preferably applied by means of Atomic Layer Deposition (ALD), the surface coating preferably containing Al2O3 or S1. dip coating, whereby the surface coating preferably contains S1O2.

Battery cell according to any one of the preceding claims, characterized in that it contains an electrode made by the following process steps: - preparation of a pasty mass of LiFePC> 4 during the possible application of a binder and / or a conductivity enhancer, - homogeneous placing the pasty mass into a three-dimensional porous metal structure, - pressing the three-dimensional metal structure containing the pasty mass in such a way as to reduce its thickness, preferably at least 20%.